Method and apparatus for enhancing aquatic environments

ABSTRACT

Submerged media useful with or without aeration and/or mixing to enhance an aquatic environment by promoting and retaining biogrowth. The media takes the form of a cluster of individual flexible elements having free ends. The media are submerged in a liquid such as a water or wastewater treatment basin or an aquaculture environment. The media are characterized by the ability to promote and retain microbial growth. The media clusters have substantial flow through thicknesses to provide a three dimensional effect along with baffling for increased contact with the liquid being treated. The media may be thin strips constructed to avoid sticking together to allow maximum exposed surface area. The media clusters can create oxic, anoxic and anaerobic environments for maximum treatment during flow through the media cluster. The flexibility of the media elements and their free ends automatically dislodges excessive biomass buildup to avoid clogging of the media.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a divisional of and claims priority to U.S. patentapplication Ser. No. 11/383,708, filed May 16, 2006, now U.S. Pat. No.7,544,286 which application is hereby incorporated by reference to theextent permitted by law.

FIELD OF THE INVENTION

This invention relates in general to the biological enhancement ofaquatic systems and deals more particularly with a method and apparatusfor enhancing aquatic environments in a manner to promote beneficialbiogrowth. Typical applications of the invention are, for example, waterand waste water treatment systems and aquaculture applications.

BACKGROUND OF THE INVENTION

Water and waste water are commonly treated using a variety ofconventional techniques. For example, waste water can be treated byaerobic, anoxic, and/or anaerobic processes, depending upon thecharacteristics of the waste water and the intended result of thetreatment. Each of these processes requires different types of bacteriaand utilizes a different mechanism for removing contaminants.Consequently, it is desirable for a treatment system to be flexible suchthat it can effect anaerobic, anoxic or an aerobic environment, eitherat different times or in different parts of the treatment system at thesame time, or by controlling system variables.

In activated sludge systems, the microbial organisms are free floatingand are circulated in the basin or other treatment reactor so that theycontact the soluble and particulate contaminants in the liquid. In othersystems the microorganisms are fixed in place and the contaminants arecirculated to them. In either case, the soluble waste and smallparticulate waste are the materials that are the primary focus oftreatment and are most difficult to remove from the liquid.

Submerged media of various types have been used to provide a base foraccumulating and growing microbial biomass in treatment basins. Rigidparallel plates and honeycomb structures allow the liquid to passbetween them and contact the biomass that accumulates on the plate andthe honeycomb cells. However, the rigidity of these structures allowsessentially unlimited buildup of biomass, so they must be cleanedfrequently or they clog unduly and disrupt the treatment operation whenused as submerged media in a high organic loading or in a low water flowenvironment. The need for frequently cleaning results in significantmaintenance costs and other problems such as down time of the treatmentfacility which limits the application of rigid systems of this type.

Other types of media have been proposed, including unusual mediaelements confined in a cage structure through which the liquid passes.Although media of this type function in a satisfactory manner in manyrespects, there are significant problems. Again, excessive biomassbuilds up on the media and must be removed frequently to preventclogging. Further, the liquid must be pumped through the media usingrelatively complex and costly pumping systems. The media is costly andtypically involves the use of baffles and other flow control devices toachieve the necessary flow pattern. Distributing the caged mediaproperly throughout the reactor also presents problems. All of thesefactors detract from the viability of caged media systems for use inmany applications.

Woven net structures have been used involving strands or other elementsstrung between support members in the reactor. These systems aredisadvantaged in that they are costly, difficult to properly distributethroughout the basin, have inadequate surface to volume ratios, and haveelements that are fixed at both ends and thus relatively inflexible sothat excess biomass can accumulate and clog the media.

The foregoing systems were developed for use as packing in towers or fortrickling filter applications where the liquid flows vertically acrossmedia surfaces and has a velocity sufficient to shear off excessbiomass. However, when they are submerged in much lower velocity basinsor lagoons with relatively slow horizontal flow and significant organicloading, the velocity is inadequate for biomass removal. Thus, thecleaning and maintenance requirements previously identified areinherent. The process control parameters in a basin or lagoon alsodiffer markedly compared to a trickling filter, and there is a need todistribute the media horizontally and vertically in a very large reactorwhich is not present in a small volume trickling filter application.

U.S. Pat. Nos. 6,060,153; 6,171,686; 6,230,654 and 6,244,218 to McNeildisclose woven fabric in the form of thin sheets used primarily inaquaculture environments. The sheets may be split in their lowerportions to form side by side strips. However, each strip is a thinplanar structure having a thickness of only about ⅛ inch or less. Thewater can pass through the slits, but each strip is essentially twodimensional so that the liquid flows quickly past the media and at mostcontacts only one strip. The strips are flexible fabric and filmsurfaces which stick together when placed close to each other. There isno three dimensional flow through effect and no baffling effect thatdirects the liquid from one media element to another. Therefore, contactbetween the particles in the liquid and the biomass on the media is noteffected in an optimal manner.

Aquacultural systems have need for waste removal as well as other needs.For example, fish and other aquatic life must be protected againstammonia contamination. The ammonia that makes its way into the watermust be converted to nitrate in a nitrification process involving onetype of biogrowth, and the nitrate may then be converted to nitrogen gasin a de-nitrification (removal) process involving different types ofmicrobes. Additionally, an environment can be provided where small fishand hatchlings are protected from predators, and the fish can utilizemuch of the biogrowth such as snails and other lower level organisms tofeed on. Proper application of submerged media allows soil or floorerosion to be stabilized where it has been allowed to occur. Theaquacultural systems proposed in the past have not adequately addressedall of these concerns.

SUMMARY OF THE INVENTION

A need remains to provide a media system that enhances the biologicalgrowth environment in various aquatic applications such as water andwaste water treatment and aquaculture systems. At the same time, themedia system must have the flexibility and adaptability in a system toallow management of the environment and the treatment process.

It is an object of the invention to provide a biogrowth media system andmethod wherein the media are arranged to present a large surface area ina controlled volume to support large biomass colonies and theaccumulation of sufficient biomass to effect the desired end result. Thetype and amount of biomass can be controlled in the system by the propercontrol of media area volume, mixing energy, aeration energy, and mediadistribution.

Another object of the invention is to provide a system and method of thecharacter described which is adapted to effect economical distributionof the media in the basin or other receptacle.

Still another object of the invention is to provide a method and systemof the character described wherein excess biomass is removedautomatically and naturally without the need to shut down the system andclean the media. This feature is achieved by providing media in the formof individual flexible elements that are free at one end so that naturalflexing of the elements causes excessive biomass to detach from themedia and drop to the bottom of the reactor.

A further object of the invention is to provide a method and system ofthe character described wherein aerobic, anoxic or anaerobic processescan be designed and operated with both low intensity lagoon wastetreatment processes and high intensity complete mix processes carriedout. Mixing with or without aeration can be selectively effected in oneor more zones to allow aerobic or anoxic or anaerobic treatment. At thesame time, the aeration/mixing can be carried out at high intensity in acomplete mix zone with clarification and/or solids return capabilities,or mixing with or without aeration can be carried out at lower intensityin lagoon systems. Also, the environment can be selected or adjusted toobtain the desired effect by changing the physical area and volumecharacteristics or the location of the media or its density, changingthe aeration location or intensity, changing the intensity of mixing, orany combination of these variables. An alternative arrangement of themedia can involve arranging the media parallel to the flow direction sothat one or more treatment channels are formed that may be beneficialfor long sludgeage applications or other special or unique applications.This flexibility sets the present invention apart from other systems andmethods and is of great practical advantage.

A still further object of the invention is to provide a method andsystem of the character described wherein the flexible media arearranged in one or more clusters with the elements collectivelyoccupying a thickness dimension to create flow through the media volumethat is substantial. Preferably this media will incorporate a thicknessof at least one inch to more than three feet in some applications. Thisthree dimensional flow through configuration is a highly importantfeature of the invention in that the particulates and solubles in theliquid are exposed to the biomass on a large number of the individualelements in each cluster, thereby maximizing the contact with thebiomass. Also, the individual elements across the thickness dimensionprovide a baffling effect causing the liquid to be directed from elementto element for further increased exposure to the biogrowth. The liquidpasses through this thickness creating concurrent oxic, anoxic, andanaerobic zones in the media volume. These zones can be controlled byaeration, mixing and proper sizing or distribution of the media.

Yet another object of the invention is to provide a method and system ofthe character described wherein the different media elements within acluster media can have different properties such as different lengths,specific gravities or other variables. For example, some elements canessentially float to provide sunlight protection, and loose or tightcompaction of the elements or long and short elements within the samecluster can be provided, thereby enhancing the versatility of the systemto meet different treatment goals.

A key characteristic of the media is the use of thin strips less thantwo inches wide to create the media cluster. These strips are speciallydesigned to minimize or eliminate any biological bonding of media andmaintain the media strips as discrete surface areas in the cluster. Thisavoids the loss of area and efficiency of flat fabric strips if placedin similar proximity to one another.

An additional object of the invention is to provide a method andapparatus of the character described which is suited to enhanceaquaculture environments. In this regard nitrification andde-nitrification can be employed alone or with other waste treatmentprocesses, and the media serves both as a support for biogrowth andmultiple life forms such as snails and other nourishment for fish and asa protected area to harbor small fish and hatchlings against predators.The system also provides stabilization where erosion in an aquaculturesystem may be a problem.

Other and further objects of the invention, together with the featuresof novelty appurtenant thereto, will appear in the course of thefollowing description.

DESCRIPTION OF THE DRAWING

In the accompanying drawing which forms a part of the specification andis to be read in conjunction therewith:

FIG. 1 is the front elevational view of a submerged media arranged in acluster in accordance with a preferred embodiment of the presentinvention.

FIG. 2 is a side elevational view of the media shown in FIG. 1;

FIG. 3 is a view similar to FIG. 2 but showing the modified submergedmedia in which the individual media elements have varying lengths inaccordance with a modified embodiment of the invention;

FIG. 4 is an elevational view similar to FIG. 2, but showing stillanother modified media in which the individual elements have varyingdensities (specific gravities) in accordance with another modifiedembodiment of the invention;

FIG. 5 is a diagrammatic elevational view showing a variety of clustersof submerged media arranged in a basin at different locations and havingdifferent characteristics;

FIG. 6 is a diagrammatic plan view of a basin or lagoon equipped withsubmerged media and other components arranged to provide different typesof treatment zones in accordance with the present invention;

FIG. 7 is a diagrammatic plan view of a basin or lagoon equipped withclusters of media that are separated by gaps in accordance with oneaspect of the present invention;

FIG. 8 is a diagrammatic plan view of a lagoon or basin equipped withsubmerged media arranged in strings or curtains extending essentiallyparallel to the direction of liquid flow of a basin or lagoon inaccordance with one aspect of the present invention;

FIG. 9 is a diagrammatic plan view of a basin or lagoon equipped withsubmerged media and other components arranged to provide complete mixaeration for combined suspended growth and media fixed film or attachedgrowth treatment in accordance with one aspect of the present invention.

DETAILED DESCRIPTION OF THE INVENTION

The present invention is directed to the use of uniquely arrangedsubmerged media to enhance the environment in an aquatic system such asa water or waste water treatment system or an aquaculture system. Thedetails of the submerged media as used in an aquatic system will bedescribed in connection with waste water treatment facilities. However,it is to be understood that the submerged media has equal applicabilityin other types of aquatic systems, including water treatment systems andaquaculture applications.

As one example of the type of aquatic environment in which the submergedmedia may be employed, FIG. 5 depicts a reactor 10 containing a liquidsuch as waste water. The reactor 10 may be a basin, lagoon or othercontainment vessel. The reactor 10 may contain a generally flat bottom12 and opposite sides 14. The liquid level of the basin 10 is identifiedby numeral 16. In accordance with the present invention, one or moreclusters 18 of submerged media may be installed in the basin 10 atsubmerged locations.

FIG. 1 depicts a cluster 18 constructed according to one embodiment ofthe present invention. The cluster 18 is constructed of a plurality ofindividual ribbons or strips 20 preferably less than two inches widewhich are bunched together to form the cluster 18. The strips 20 may besupported from a support structure that includes a cable or rope 22stretched across the basin 10 near the water line 16 and anchored to theopposite sides 14 by suitable anchors 24 (see FIG. 5). Referring againto FIG. 1 in particular, the upper ends of the ribbons 20 may be securedto a pipe or other support 26 (or to the cable 22 or a rope or otherstructure) and secured in place by clamps 28.

With additional reference to FIG. 2, the strips 20 are folded over thesupport cable or rope at 20 a and secured to the rope or cable or topipe 26 in any suitable manner. The strips have free lower ends 20 bwhich are submerged well below the water level 16 and which areunattached so that the strips 20 are free to flex or flutter. As shownin FIGS. 1 and 2, the strips are preferably arranged closely togetheralong a length dimension L (FIG. 1) of the cluster 18. The lengthdimension L may occupy the entire width of the basin or some distanceless than the basin width. Each cluster 18 has a thickness dimension T(FIG. 2) that may vary to match process needs. The thickness dimension Tis occupied by a plurality of the individual strips 20 and preferably isat least one inch thick and may be up to three feet thick or more insome applications. In any event, the thickness dimension T should besubstantial so that the liquid that is being treated will be exposed toa relatively large number of strips 20 as the liquid passes through thethickness T. The media clusters allow the design of systems with oxic,anoxic and anaerobic environments as waste passes through the clusters.The bunching of the strips 20 throughout the thickness dimension T alsoarranges the strips such that they have a baffling effect to increasethe distribution and exposure of the liquid to the surfaces of thediscrete strips 20 as the liquid passes through the thickness dimensionT. The strips 20 are constructed and arranged to prevent them fromsticking together, even when biomass builds up on them. This maintainseach strip as an individual discrete element for enhanced effectiveness.By way of example, the strips 18 can be curved, heated and twisted, orotherwise constructed in a manner to resist lying flatly against oneanother, although the invention contemplates flat as well as otherconfigurations.

FIG. 3 depicts a cluster 18 in which the strips include relatively longstrips having their lower ends 20 b located well below the ends 21 b ofshorter strips 21. It should be understood that the strips in any mediacluster 18 may have various lengths and may be compacted to provide eachcluster with different densities or compactions and thicknessdimensions.

The arrangement shown in FIG. 4 depicts a somewhat modified cluster 18in which some shorter strips 21 have a lower specific gravity or morebuoyant than the higher density strips 20. Consequently, the strips 21may float on or near the liquid surface 16 and thus act to blocksunlight from reaching the underlying cluster 18 and the strips 20contained therein.

Referring again to FIG. 5, some or all of the clusters 18 may besupported on a cable 30 or other submerged support located well belowthe liquid level 16. The cable 30 may be connected at its opposite endwith submerged anchors 32 located on the sides 14 at a location spacedabove the bottom 12 but below the water line 16. Some of the clusters 18supported on the cable 30 may have a specific gravity greater than 1.0such that the ribbons 20 hang downwardly from the cable 30. Otherclusters 18 may include individual ribbons 23 having specific gravitiesequal to or less than 1.0 such that the free ends 23 b of strips 23 areat the upper ends of the clusters as the buoyant media ribbons 23 tendto rise in the reactor 10. Combinations of long and short ribbons can beused in any of the clusters 18. Likewise, ribbons having variousspecific gravities can be used in any of the clusters 18. The ribbons inany of the clusters 18 may be installed densely or loosely or anywherein between.

With continued reference to FIG. 5, the submerged media clusters 18 maybe used with an aeration system. The aeration system may include afloating air lateral (pipe) 34 which is located at the water level 16and secured in place at its opposite ends. One end of the air lateral 16receives air under pressure from a blower 36. Aeration devices which maytake the form of submerged tubular diffusers 38 may be suspended fromthe air lateral 34 on flexible hoses 40. The diffusers 38 are preferablylocated slightly above the bottom 12 of the reactor 10 and function in awell known manner to diffuse air into the liquid in the reactor vesselin the form of fine bubbles which provide aeration and circulation ofthe liquid. It should be understood that other types of aeration devicescan be employed in connection with the submerged media, including floormounted or surface mounted aerators. The diffusers 38 may be selectivelyoperated (supplied with air) in order to aerate the liquid at such timesand such intensities and durations as is appropriate for the particularresult that is desired.

Preferably, the individual strips 20 take the form of thin members lessthan two inches wide that may be constructed of a flexible plastic suchas polyethylene or other synthetic material, as well as a wide varietyof other materials. The material used should be characterized by theability to effectively promote the growth of microbes and to allow thebiogrowth to accumulate on the strips in sufficient quantity toeffectively treat the wastewater or other liquid that is undergoingtreatment. At the same time, the flexibility of the strips 20 andmaintaining one end 20 b (or 21 b or 23 b) free allows the strips 20 tonaturally flex when wastewater flows through the clusters 18, with theflexing of the strips acting to dislodge excessive biomass that mayaccumulate on them. In this manner, undue buildup of biomass that couldclog the clusters 18 is avoided. The strips may also be shaped toprevent bio-bonding in order to maintain full function when partially orfully loaded with biomass.

Alternatively, the strips may be constructed of a variety of materialsand may have configurations other than flat strips. By way of example,human or animal hair, synthetic fibers, suspended ropes, woven strings,woven fabrics or sheets or ribbons of various materials may be used, asmay other elements that are suitably flexible and capable of beingsupported adequately in an aquatic environment without bio-bonding.Whatever exact type of flexible element is used, the elements should bearranged in clusters having a significant thickness dimension T toprovide a three dimensional flow through effect of the treatment, aspreviously described.

FIGS. 6-9 depict various wastewater treatment applications in which thesubmerged media may be used in accordance with the present invention.Referring first to FIG. 6, a basin or lagoon 110 is provided with aplurality of clusters 18 of the submerged media. The clusters 18 mayeach extend in a substantially continuous curtain across the entirewidth of the basin or lagoon 110. The wastewater flow is longitudinallythrough the length of the basin 110, as indicated by the directionalarrows 112 at the inlet end of the basin or lagoon. Flows along andthrough the media are typically assisted by operation of an aerationsystem.

The basin or lagoon 110 may be provided adjacent to its inlet end with azone 114 which may be anoxic or anaerobic. The zone 114 may be providedwith a mixing device 116 that is non-aerating. The zone 114 may beprovided with one or more of the media clusters 18 (or no submergedmedia in some cases). The basin or lagoon 110 may be provided withanother zone 120 downstream from zone 114 which may include one or moreof the submerged media clusters 18 and/or one or more aeration chains122. The clusters 18 may be arranged in a continuous curtain extendingtransversely across the basin or lagoon 110. The aeration strings 122may each take a form similar to what is shown in FIG. 5 and may includesubmerged tubular diffusers 38 or other suitable aeration devices. Anoptional recirculation line 124 may be provided to extend from theoutlet end of the basin 110 back to the inlet end.

In operation of the system shown in FIG. 6, the incoming wastewaterenters the basin or lagoon in the first zone 114 which may be an anoxicor anaerobic zone for anoxic or anaerobic treatment of the wastewater atthe inlet end portion of the basin. The wastewater then flows into thesecond zone 120 which may be operated as an anoxic zone (with little orno aeration) or as a low or high level aerobic zone if the aerationchains 122 are operated with high intensity aeration. A third zone issometimes employed for maximum process control.

In the system of FIG. 6 or any other system employing the submergedmedia, the wastewater or other liquid that is being treated flowsthrough the cluster 18 at a relatively slow rate. The wastewater isexposed to the microbial biomass that grows and accumulates on theindividual strips 20 or other flexible elements in the cluster 18 suchthat the microbes are able to remove suspended and soluble solids. Theprovision of a substantial thickness dimension T in each cluster 18results in significant exposure of the liquid to the biomass because theliquid is directed in intimate contact with a number of different strips20 as it flows through the thickness dimension T. In addition, thestrips 20 have a baffling effect which directs the wastewater from stripto strip to increase the exposure and contact time of the liquid withthe biomass.

It is a particular feature of the invention that the flexibility of theindividual flexible elements in each cluster 18 results in the elementsbeing naturally flexed by aeration/mixing or the wastewater flowingthrough the clusters 18, with the flexure being allowed due to the freeends of the flexible elements in the cluster and the special non-stick(non bio-bond) construction thereby automatically dislodging any excessbiomass build up that may occur on the elements in the cluster. Thisautomatic dislodging of excessive biomass prevents the clusters 18 fromclogging unduly and inhibiting the flow of wastewater through theclusters to lose treatment efficiency and the maintenance problems thatplague other types of submerged media are thus avoided, along with thecosts and downtime associated with such maintenance requirements.

With reference to FIG. 7, a basin or lagoon 210 receives wastewater atits inlet end, as indicated by the directional arrow 212. The basin 210is equipped with a plurality of clusters 18 of submerged media which arearranged in strings extending transversely across the width of the basinor lagoon 210 perpendicular to the flow direction. In each string ofmedia, one or more gaps 214 may be presented between adjacent clusters.Optional aerators 216 may be located to provide aeration in some or allof the gaps 214 if desired. The gaps in adjacent strings of submergedmedia clusters 18 may be staggered or offset from one another, asindicated for the gaps 214 a and 214 b. The submerged media may bearranged with gaps in an application of the type shown in FIG. 6 or anyother configuration, depending upon the desired treatment.

FIG. 8 depicts a basin or lagoon 310 which receives incoming wastewaterat its inlet end as indicated by the directional arrows 312 whichindicate the direction of flow longitudinally in the basin 310. One ormore strings of submerged media clusters 18 are installed in the basinor lagoon 310 to extend longitudinally in a direction substantiallyparallel to the direction of flow indicated by the directional arrow312. The clusters 18 may be arranged to extend continuously in a curtainextending the entire length of the basin or lagoon 310, or the clustersmay be arranged with gaps in each string of submerged media. Betweeneach adjacent pair of strings of submerged media 18, a channel 314 isformed for the flow of wastewater from the inlet and to the outlet endof the basin or lagoon 310. One or more of the channels 314 may beequipped with an aeration chain 316 arranged with the aerators 38 spacedapart in a direction longitudinally of the basin along the length of thechannel 314. The aeration devices of the aeration chain 316 may betubular diffusers such as those identified by numeral 38 in FIG. 5, orother types of aeration devices. The arrangement of FIG. 8 may find usein some long sludgeage applications or in other special applicationsinvolving the treatment of wastewater or other liquids.

FIG. 9 depicts a lagoon 410 that is equipped with submerged media incombination with a suspended biogrowth system. Wastewater enters thebasin or lagoon 410 at its inlet end and flows longitudinally throughthe basin in the direction indicated by the directional arrow 412. Theinlet end portion of the basin or lagoon 410 may be arranged to providea complete mix zone 414. In zone 414, one or more strings of submergedmedia clusters 18 may be provided. The submerged media clusters 18 maybe oriented to extend either longitudinally in the complete mix zone 414or transversely in zone 414. Preferably, an aeration chain 416 isprovided between each adjacent pair of strings of clusters 18. Theaeration chains 416 may extend parallel to the clusters 18 and mayinclude tubular diffusers 38 or other suitable aeration devices.

A clarifier 418 or other solids separation device may be provided toeffect settling of sludge from the liquid in the basin 410. Selectedquantities of sludge 420 may be returned to the head end of the basin410 along a sludge return line 420.

Downstream from the complete mix zone 414, the basin may be equippedwith additional strings of clusters 18 and/or additional aeration chains416. The strings of clusters 18 may be arranged and oriented invirtually any manner, as may the aeration chains 416.

The aeration in the complete mix zone 414 is carried out with sufficientintensity to maintain a complete mix condition in zone 414. Downstreamzones are typically operated under partial mix conditions.

From the foregoing it will be seen that this invention is one welladapted to attain all ends and objects hereinabove set forth togetherwith the other advantages which are obvious and which are inherent tothe structure.

It will be understood that certain features and subcombinations are ofutility and may be employed without reference to other features andsubcombinations. This is contemplated by and is within the scope of theclaims.

Since many possible embodiments may be made of the invention withoutdeparting from the scope thereof, it is to be understood that all matterherein set forth or shown in the accompanying drawings is to beinterpreted as illustrative, and not in a limiting sense.

1. A process for providing an environment conducive to biogrowth in anaquatic system, comprising: installing in the aquatic system a pluralityof flexible elements arranged in at least one cluster wherein saidelements collectively occupy a thickness dimension of at least about oneinch and at least one cluster extends in a substantially continuouscurtain across substantially the entirety of the width of the aquaticsystem, said elements being characterized by the ability to promote thegrowth and accumulation of microbes thereon; maintaining one end of saidelements free to allow flexing of said elements for dislodging ofexcessive biomass therefrom; and aerating selected areas of the aquaticsystem.
 2. A process as set forth above in claim 1, including mixing aselected volume of the aquatic system without aeration thereof to effectanoxic or anaerobic conditions therein, said selected volume having atleast one of said clusters therein.
 3. A process as set forth in claim1, wherein said selected areas are located at gaps between a pluralityof said clusters.
 4. A process as set forth in claim 1, wherein saidstep of installing comprises arranging said cluster to extend generallytransverse to the direction of flow in said aquatic system.
 5. A processas set forth in claim 4, wherein a plurality of said clusters arearranged in generally parallel rows and said selected areas are betweenadjacent rows of said clusters.
 6. A process as set forth in claim 1,wherein said elements are arranged in a plurality of clusters and saidstep of installing comprises arranging at least one of said clusters toextend generally parallel to the direction of flow in said aquaticsystem.
 7. A process as set forth in claim 6, wherein a plurality ofsaid clusters are arranged in generally parallel rows and said selectedareas are between adjacent rows of said clusters.
 8. A process as setforth in claim 1, wherein: said selected areas include a complete mixzone; and aerating said complete mix zone comprises effecting a completemix condition of solids in said complete mix zone.
 9. A process as setforth in claim 1, wherein flow through said thickness dimension effectsoxic conditions.
 10. A process as set forth in claim 9, wherein flowthrough said thickness dimension effects anoxic conditions.
 11. Aprocess as set forth in claim 10, wherein flow through said thicknessdimension effects anaerobic conditions.
 12. A process as set forth inclaim 9, wherein flow through said thickness dimension effects anaerobicconditions.
 13. A process as set forth in claim 1, wherein flow throughsaid thickness dimension effects anoxic conditions.
 14. A process as setforth in claim 13, wherein flow through said thickness dimension effectsanaerobic conditions.
 15. A process as set forth in claim 1, whereinflow through said thickness dimension effects anaerobic conditions. 16.A process as set forth in claim 1, wherein said at least one clusterincludes: a first zone for effecting at least one of anoxic, anaerobicand aerobic treatment of a liquid within the aquatic system, and asecond zone for effecting at least another of anoxic, anaerobic andaerobic treatment of the liquid within the aquatic system.
 17. A processas set forth in claim 1, wherein said step of aerating promotes theflexing of said elements for dislodging excessive biomass therefrom. 18.A process as set forth in claim 1, wherein said elements hang downwardlyfrom a cable and have a lower free end.
 19. A process as set forth inclaim 18, wherein said step of aerating includes installing an aerationdevice proximate an upper end of said at least one cluster.
 20. Aprocess as set forth in claim 19, wherein said aeration device is afloating aeration device.
 21. A process for providing an environmentconducive to biogrowth in an aquatic system, comprising: installing inthe aquatic system a plurality of flexible elements arranged in aplurality of clusters wherein said elements collectively occupy athickness dimension of at least about one inch, said elements beingcharacterized by the ability to promote the growth and accumulation ofmicrobes thereon; maintaining one end of said elements free to allowflexing of said elements for dislodging of excessive biomass therefrom;and aerating selected areas of the aquatic system, wherein said selectedareas include a complete mix zone having a plurality of said clustersinstalled therein and a second zone downstream from said complete mixzone having a plurality of said clusters installed therein; and whereinaerating said complete mix zone comprises effecting a complete mixcondition of solids in said complete mix zone.
 22. A process forenhancing an aquaculture system in which aquatic life exists in water,said process comprising: installing in the water a medium having aplurality of individual flexible elements characterized by the abilityto promote microbial growth thereon and arranged in a cluster whereinsaid elements collectively occupy a thickness dimension of at leastabout one inch and the cluster extends in a substantially continuouscurtain across substantially the entirety of the width of theaquaculture system, said elements having free lower ends allowing saidelements to flex for dislodging of excessive biomass therefrom; andaerating the water near said medium.